JPS6223524Y2 - - Google Patents

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Publication number
JPS6223524Y2
JPS6223524Y2 JP1983113166U JP11316683U JPS6223524Y2 JP S6223524 Y2 JPS6223524 Y2 JP S6223524Y2 JP 1983113166 U JP1983113166 U JP 1983113166U JP 11316683 U JP11316683 U JP 11316683U JP S6223524 Y2 JPS6223524 Y2 JP S6223524Y2
Authority
JP
Japan
Prior art keywords
water
tank
water intake
flow
solid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP1983113166U
Other languages
Japanese (ja)
Other versions
JPS6021310U (en
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to JP11316683U priority Critical patent/JPS6021310U/en
Publication of JPS6021310U publication Critical patent/JPS6021310U/en
Application granted granted Critical
Publication of JPS6223524Y2 publication Critical patent/JPS6223524Y2/ja
Granted legal-status Critical Current

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  • Farming Of Fish And Shellfish (AREA)
  • Physical Water Treatments (AREA)

Description

【考案の詳細な説明】 本考案者は、〓に、水平回転セン断流れの中に
置かれた固体は求心運動をすることを利用して、
液体中に含まれている固体を連続的に分離する方
法を発明(特開昭54−61363号)したものである
が、本考案はその改良考案である。
[Detailed description of the invention] The inventor of the present invention made use of the fact that a solid placed in a horizontally rotating shear flow moves centripetally.
A method for continuously separating solids contained in a liquid was invented (Japanese Unexamined Patent Publication No. 54-61363), and the present invention is an improved version of that method.

本考案による分離槽は流れのある状態において
連続的に大量の原水を固液分離するものであり、
従来の沈澱池方式とは原理を異にしている全く新
しいものである。
The separation tank according to the present invention continuously separates a large amount of raw water into solid and liquid in a flowing state.
This is a completely new system that differs in principle from the conventional sedimentation tank system.

以下、本考案の実施例を図面につき説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図中、1は水槽であつて、第1図Aに図示の如
き円形水槽または第1図Bに図示の如き角形水槽
が実施例として示される。第1図A,Bと第2図
に示すように水槽1中に、その上部内では中心部
分の流れが遅く周辺部での流れは速いと云う水平
回転セン断流れを生成せしめるように、原水を水
槽1の水面4に近接した上半分の処で(実用上
は、原水流入管5の中心位置を水槽1の水深Hの
3/4乃至1/2の処となして)水槽周辺より原水流入
管5,5,5を介して円周方向に流入せしめる。
即ち、該流入管5,5は水槽周辺に接線方向に設
けるのである。而して、水槽1中心位置に上端開
口の取水管8を直立せしめ、該取水管8の上端に
取水盤9を設け、該取水盤9上に連結体14を介
して水面4に浮ぶフロート11を設けて取水する
ようにする。図中、15は取水盤9の周辺部の
(水面に平行な)水平部である。該連結体14
は、図示の通り、螺杆12とボルト13とより成
り、取水口6の上下方向の開口寸法を調節し得る
位置に応じて伸縮し得るものとする。水槽底部に
はその中央部に漏斗状の固形物含有水の排出口7
を設ける。而して、より最上の効果を上げるため
には、液体中に含まれる固形分の大きさ、比重、
液体の粘性等に合わせて水槽の大きさ、回転流の
流速、流入角度、水槽の深さ、水槽底部の底面の
傾斜角を決めるものとする。
In the figure, reference numeral 1 denotes an aquarium, and a circular aquarium as shown in FIG. 1A or a rectangular aquarium as shown in FIG. 1B are shown as examples. As shown in Figures 1A and B and Figure 2, the raw water is fed into the water tank 1 so as to generate a horizontally rotating shear flow in which the flow in the upper part of the tank 1 is slower in the center and faster in the periphery. in the upper half of the water tank 1 close to the water surface 4 (in practice, the center position of the raw water inflow pipe 5 should be set at the water depth H of the water tank 1).
The raw water is allowed to flow in from the periphery of the water tank in the circumferential direction via inlet pipes 5, 5, 5 (3/4 to 1/2).
That is, the inflow pipes 5, 5 are provided tangentially around the water tank. Thus, a water intake pipe 8 with an open top end is erected at the center of the water tank 1, a water intake board 9 is provided at the upper end of the water intake pipe 8, and a float 11 floating on the water surface 4 is placed on the water intake board 9 via a connecting body 14. A system will be installed to take in water. In the figure, 15 is a horizontal part (parallel to the water surface) around the water intake board 9. The connecting body 14
As shown in the figure, it is made up of a screw rod 12 and a bolt 13, and can expand and contract depending on the position where the vertical opening size of the water intake port 6 can be adjusted. At the bottom of the tank, there is a funnel-shaped outlet 7 for water containing solids in the center.
will be established. Therefore, in order to achieve the best effect, it is necessary to adjust the size and specific gravity of the solid content contained in the liquid.
The size of the tank, the flow rate of the rotating flow, the inflow angle, the depth of the tank, and the angle of inclination of the bottom of the tank shall be determined according to the viscosity of the liquid.

第3図は前記の水槽を多段に組合せて連結配管
したものを示す。第一段目の固液分離槽1の取水
口6および固形物含有水の排出口7からの水を、
夫々第二段目の(二個の)固液分離槽2,3に対
する原水の流入口5′,5″に、直接に又は固形分
離槽10を介して、流入させるように多段に接続
させたものである。これ等の二段目の固液分離槽
2,3からの四種類の水は夫々第三段目の(四個
の)固液分離槽(図示しない)に至るものであ
る。之に依り、固形物と水との分離が益々良いも
のが得られる。
FIG. 3 shows the above-mentioned water tanks combined in multiple stages and connected with piping. The water from the water intake port 6 and solid matter-containing water discharge port 7 of the first-stage solid-liquid separation tank 1 is
The raw water was connected to the inlets 5' and 5'' of the second-stage (two) solid-liquid separation tanks 2 and 3, respectively, in a multi-stage manner so as to flow directly or through the solid-liquid separation tank 10. The four types of water from these second-stage solid-liquid separation tanks 2 and 3 reach the third-stage (four) solid-liquid separation tanks (not shown), respectively. As a result, even better separation of solids and water can be obtained.

本考案は、前記のように、取水口部を盤状とな
すと共に原水流入管5の水槽1への開口位置の水
深hを、水槽の水深をHとして、h=(3/4〜1/2
)H となしたことにより、水槽1内で砂などの沈澱物
が巻き上がることの阻止、及び水面4附近への砂
などの固体粒子の浮遊の防止が適確に行われ、固
形物と水との分離を能率的に行うまことに合理的
な装置を経済的に得たものである。本考案は、水
力発電所に於ける従来の沈澱池の代りとして著し
く小型な排砂装置としても優れたものである。原
水流入管5の中心位置の水深hを1/2Hよりも少
ならしめるときは、水槽1の下半部に集められた
砂などの沈澱物を巻き上がらせる虞れがあり固液
分離に悪影響を及ぼす。また、水深hを3/4Hよ
り大ならしめるときは、水槽1の水面4附近で取
水される水の中に直接原水が混入し砂などの粒子
(固体)を混入させる虞れがあり好ましくないの
である。依つて、実用上は h=(3/4〜1/2)H とするのである。
As mentioned above, in the present invention, the water intake port is plate-shaped, and the water depth h at the opening position of the raw water inflow pipe 5 to the water tank 1 is defined as h = (3/4 to 1/2 2
)H, it is possible to accurately prevent sediment such as sand from being stirred up in the water tank 1, and to prevent solid particles such as sand from floating near the water surface 4, thereby preventing solid matter and water. This is an economical and truly rational device that efficiently performs the separation. The present invention is also excellent as an extremely compact sand removal device that can be used as a replacement for conventional settling basins in hydroelectric power plants. When the water depth h at the center position of the raw water inflow pipe 5 is made less than 1/2H, there is a risk that sediment such as sand collected in the lower half of the water tank 1 will be rolled up, which will have a negative effect on solid-liquid separation. effect. In addition, when the water depth h is made larger than 3/4H, it is not preferable because there is a risk that the raw water will directly mix into the water taken near the water surface 4 of the water tank 1, and particles (solids) such as sand may be mixed in. It is. Therefore, in practice, h=(3/4 to 1/2)H.

前記のように、原水流入管5の中心位置の水深
hは、水槽の水深Hに対し h=(3/4〜1/2)H となるようにする。第2図図示のものは h≒3/5H である。
As mentioned above, the water depth h at the center position of the raw water inflow pipe 5 is set to be h=(3/4 to 1/2)H with respect to the water depth H of the water tank. In the case shown in Fig. 2, h≒3/5H.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本考案に係る固液分離槽の実施例を示し
たものであつて、第1図A、第1図Bは夫々円形
水槽、角形水槽の実施例を示した平面図、第2図
は第1図Aのものゝ断面側面図、第3図は多段式
に水槽を組合せて連結配管したフローシート、で
ある。 1は水槽、2,3は第二段目の水槽、4は水
面、5は原水流入管、6は取水口、7は固形物含
有水の排出口、8は取水管、9は取水盤、10は
固形物分離槽、11はフロート、12は螺杆、1
3はボルト、14は連結体。
The drawings show an embodiment of the solid-liquid separation tank according to the present invention, and FIG. 1A and FIG. 1B are plan views showing the embodiments of a circular water tank and a square water tank, respectively, and FIG. Fig. 1A is a cross-sectional side view, and Fig. 3 is a flow sheet in which water tanks are combined in a multi-stage manner and connected with piping. 1 is a water tank, 2 and 3 are second stage water tanks, 4 is a water surface, 5 is a raw water inflow pipe, 6 is a water intake port, 7 is an outlet for solids-containing water, 8 is a water intake pipe, 9 is a water intake board, 10 is a solid separation tank, 11 is a float, 12 is a screw rod, 1
3 is a bolt, 14 is a connecting body.

Claims (1)

【実用新案登録請求の範囲】 水槽1中に、その上部内では中心部分での流れ
が遅く周辺部での流れは速いと云う水平回転セン
断流れが全面的に生成され且つ水槽下部では水平
回転セン断流れが弱くなるように、原水を流入せ
しめる原水流入管5,5を水槽周辺に接線方向に
設けると共に、水槽1中心位置に上端開口の取水
管8を直立せしめ、該取水管8の上端に、水面4
に浮ぶフロート11に吊支された取水手段を設け
て取水するようにした固液分離槽装置に於て、 前記取水手段は、盤状の取水盤9に取水口6の
ある取水手段であると共に、前記原水流入管5の
中心位置の水深hは、水槽1の水深Hに対し、 h=(3/4〜1/2)H であることを特徴とする固液分離槽装置。
[Claim for Utility Model Registration] In the upper part of the tank 1, a horizontally rotating shear flow is generated, in which the flow is slow in the center and fast in the periphery, and horizontally rotating in the lower part of the tank. In order to weaken the shedding flow, raw water inflow pipes 5, 5 for raw water to flow in are provided tangentially around the water tank, and a water intake pipe 8 with an opening at the top is erected at the center of the water tank 1, and the upper end of the water intake pipe 8 is To, water surface 4
In a solid-liquid separation tank device in which water is taken in by providing a water intake means suspended on a float 11 floating on the ground, the water intake means is a water intake means having a water intake port 6 on a disk-shaped water intake plate 9, and , A solid-liquid separation tank device characterized in that the water depth h at the center position of the raw water inflow pipe 5 is h=(3/4 to 1/2)H with respect to the water depth H of the water tank 1.
JP11316683U 1983-07-22 1983-07-22 Solid-liquid separation tank using rotating shear flow Granted JPS6021310U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11316683U JPS6021310U (en) 1983-07-22 1983-07-22 Solid-liquid separation tank using rotating shear flow

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11316683U JPS6021310U (en) 1983-07-22 1983-07-22 Solid-liquid separation tank using rotating shear flow

Publications (2)

Publication Number Publication Date
JPS6021310U JPS6021310U (en) 1985-02-14
JPS6223524Y2 true JPS6223524Y2 (en) 1987-06-16

Family

ID=30262067

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11316683U Granted JPS6021310U (en) 1983-07-22 1983-07-22 Solid-liquid separation tank using rotating shear flow

Country Status (1)

Country Link
JP (1) JPS6021310U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011072904A (en) * 2009-09-30 2011-04-14 Sekisui Chem Co Ltd Solid-liquid separator and water treatment apparatus

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3721004B2 (en) * 1999-04-14 2005-11-30 株式会社神鋼環境ソリューション Biological water treatment apparatus and biological water treatment method
KR100665826B1 (en) 2006-04-07 2007-01-10 김현기 A drinking water purifying apparatus

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5461363A (en) * 1977-10-21 1979-05-17 Kunihiro Ogiwara Solid*liquid separation tank using rotary cutting flow

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5286876U (en) * 1975-12-25 1977-06-29

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5461363A (en) * 1977-10-21 1979-05-17 Kunihiro Ogiwara Solid*liquid separation tank using rotary cutting flow

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011072904A (en) * 2009-09-30 2011-04-14 Sekisui Chem Co Ltd Solid-liquid separator and water treatment apparatus

Also Published As

Publication number Publication date
JPS6021310U (en) 1985-02-14

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